• 제목/요약/키워드: Overall transfer coefficient

검색결과 267건 처리시간 0.026초

An analytical model to decompose mass transfer and chemical process contributions to molecular iodine release from aqueous phase under severe accident conditions

  • Giedre Zablackaite;Hiroyuki Shiotsu;Kentaro Kido;Tomoyuki Sugiyama
    • Nuclear Engineering and Technology
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    • 제56권2호
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    • pp.536-545
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    • 2024
  • Radioactive iodine is a representative fission product to be quantified for the safety assessment of nuclear facilities. In integral severe accident analysis codes, the iodine behavior is usually described by a multi-physical model of iodine chemistry in aqueous phase under radiation field and mass transfer through gas-liquid interface. The focus of studies on iodine source term evaluations using the combination approach is usually put on the chemical aspect, but each contribution to the iodine amount released to the environment has not been decomposed so far. In this study, we attempted the decomposition by revising the two-film theory of molecular-iodine mass transfer. The model involves an effective overall mass transfer coefficient to consider the iodine chemistry. The decomposition was performed by regarding the coefficient as a product of two functions of pH and the overall mass transfer coefficient for molecular iodine. The procedure was applied to the EPICUR experiment and suppression chamber in BWR.

비 등온 유한요소해석을 위한 접면열전달계수의 결정

  • 강연식;양동열
    • 한국정밀공학회:학술대회논문집
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    • 한국정밀공학회 1996년도 춘계학술대회 논문집
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    • pp.783-786
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    • 1996
  • In the temperature analysis, the heat transfer between the workpiece and the die has an important influence upon the temperature distribution. The accuracy of thermal analysis depends on the proper description of boundafy conditions. A t the contact surface of two materials with different temperature, this requires the knowledge of overall heat transfer coefficients. In order to evaluate the overall heat transfer coefficients, a technique is developed. This technique involves temperature measurement at the contact surface during hot upsetting operations and finite element computation to calcualte the overall heat transfer coefficient.

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젖은 벽탑을 이용한 디에틸렌트리아민과 디에틸에탄올아민 수용액의 CO2 흡수속도 측정 (Kinetics of CO2 Absorption in Aqueous DETA and DEEA Solutions by Wetted-Wall Column)

  • 유정균;이준;홍연기
    • Korean Chemical Engineering Research
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    • 제60권4호
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    • pp.582-587
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    • 2022
  • 연소 배가스 중 CO2를 포집하기 위한 에너지 저감형 흡수제로 상분리 흡수제가 주목 받고 있다. 본 연구에서는 2종의 아민을 혼합한 상분리 흡수제 중 하나인 디에틸렌트리아민(diethylenetriamine, DETA)과 디에틸아미노에탄올(diethylaminoethanol, DEEA) 흡수제를 구성하는 DETA와 DEEA 각각의 흡수 속도를 측정하기 위해 젖은 벽탑을 사용하였다. 총괄 물질전달 계수에 대한 DETA 및 DEEA의 농도와 조업 온도에 따른 영향을 고찰하였다. 그 결과 DETA 농도에 따라 총괄 물질전달 계수는 비례하였지만 DEEA 농도의 경우 그 영향이 적었고 일정 농도를 넘어설 경우 총괄 물질전달 계수가 감소하였다. DETA 수용액은 조업 온도에 따라 총괄 물질전달 계수의 변화가 적었던 반면 DEEA 수용액은 조업 온도에 따라 총괄 물질전달 계수가 증가하였다. 의사 1차 반응 가정 하에서 관찰 반응 속도 상수를 구한 결과 DETA 수용액에서의 관찰 반응속도 상수는 DETA 농도에 따라 비례하는 관계를 가지나 DEEA는 의사 1차 반응 가정에 맞지 않는 것으로 나타났다.

수평 평활관내에서 비공비혼합냉매의 강제대류 증발열전달 (Forced Convective Evaporating Heat Transfer of Non-azeotropic Refrigerant Mixtures in a Horizontal Smoothed Tube)

  • 박기원;오후규
    • 설비공학논문집
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    • 제7권2호
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    • pp.225-233
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    • 1995
  • Experiments were performed to investigate the heat transfer characteristics of nonazeotropic mixture R-22+R-114 in a heat pump system. The ranges of parameter, such as heat flux, mass flow rate, and quality were $8,141{\sim}32,564W/m^2$, 24~58kg/h, and 0~1, respectively. The overall compositions of the mixtures were 50 and 100 per-cent of R-22 by weight for R-22+R-114 mixture. The results indicated that there were distinct different heat transfer phenomena between the pure substance and the mixture. In case of pure refrigerant the heat transfer rates for cooling were strongly dependent upon quality of the refrigerant. Overall evaporating heat transfer coefficients for the mixture were somewhat lower than pure R-22 values in the forced convective boiling region. For a given flow rate, the heat transfer coefficient at the circumferential tube wall(top, side, and bottom of the test tube) for R-22/R-114(50/50wt%)mixture, however, was higher than for pure R-22 at side and bottom of the tube. Furthermore, a prediction for the evaporating heat transfer coefficient of the mixtures was developed based on the method of Yoshida et.al.'s. The resulting correlation yielded a good agreement with the data for the refrigerant mixtures.

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A Review on the Performance of Fin-and-Tube Heat Exchangers Under Frosting and Defrosting Conditions

  • Kim, Yong-Chan;Lee, Ho-Seong
    • International Journal of Air-Conditioning and Refrigeration
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    • 제13권3호
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    • pp.152-157
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    • 2005
  • This paper reviews the literature on the performance of fin-and-tube heat exchangers under frosting and defrosting conditions. The effects of frosting and defrosting on the following parameters were discussed: frost growth, overall heat transfer coefficient, surface roughness, and surface characteristics on the heat exchanger. Comparisons of the experimental results and empirical correlations that were obtained from open literature were presented. In addition, a review of the defrosting methods was conducted.

비공비혼합냉매를 사용하는 열펌프의 응축열전달 특성 (Condensing Heat Transfer Characteristics on a Heat Pump System Using Non-Azeotropic Refrigerant Mixtures)

  • 박기원;오후규;김욱중
    • 대한기계학회논문집
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    • 제19권4호
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    • pp.1125-1133
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    • 1995
  • Experiments were performed to investigate the condensing heat transfer characteristics of non-azeotropic mixtures of R-22 and R-114 in a heat pump system with a horizontal smooth tube as a condenser. The ranges of parameters, such as heating capacity, mass flow rate of refrigerant and quality were 780-3,480W, 24-71kg/h, and 0-1, respectively. The overall compositions of R-22 in a R-22/114 mixture were 25, 50, 75 and 100 per cent by wight. The results show that the overall condensing heat transfer coefficients for the mixtures were lower than the pure R-22 values. Local heat transfer coefficient of the pure R-22 was hghest at the top of the test tube. The local heat transfer coefficient of R-22/114 (50/50 wt%) at side and bottom of the test tube was higher than that at the top. From the obtained data, a prediction for the condensing heat transfer coefficients of the mixture was done based on the method of Fujii.

반용융 단조에서 가압 단계가 제품에 미치는 영향 (The Influence of Compression Step on Products for Semi-Solid Forging)

  • 최재찬;박형진;이병목
    • 소성∙가공
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    • 제7권2호
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    • pp.139-149
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    • 1998
  • The technology of Semi-Solid Forging(SSF) has been actively developed to fabricate near net shape products using light and hardly formable materials. Generally the SSF process is composed of slug is compressed during a certain holding time in order to completely fill the die cavity and accelerate the solidification rate. The decision of compression time is important since it can affect microstructural characteristics, mechanical properties and shape of products.. In order to determine it proper overall heat transfer coefficient between the slug and dies should be investigated. This paper presents the procedure to find the overall heat transfer coefficient between the slug and dies by nonlinear optimization of temperature and solid fraction for a cylindrical slug at compression step in closed-die semi-solid forging. In finite ele-ment heat transfer analysis release of latent heat during solidification was considered. The influence of the predicted compression time on miscrostructural characteristics mechanimcal properties and shape of products is finally investigated by experiment.

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바이오가스용 소형 열교환기 연구 (Compact Heat Exchanger Design for Biogas Application)

  • 이택홍;김태완;박태성;강영진;노재현
    • 한국수소및신에너지학회논문집
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    • 제25권2호
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    • pp.183-190
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    • 2014
  • Our lab designs a heat exchangers for air and carbondioxide gas. Coolant is water, thus it is very difficult to determine heat transfer parameters in this gas-liquid system. Repeated experiments gives overdesign value 35%, overall heat transfer coefficient $33.8(kcal/m2-hr-^{\circ}C)$ for carbondioxide. Another series of experiments determine overdesign 18.7%, overall heat transfer coefficient $21.4(kcal/m2-hr-^{\circ}C)$ for Air. These parameters are in same range of literature. Overdesign is increasing as tube length increases, also increases as wall thickness of heat exchanger increases. To get proper fluid linear velocity in heat exchanger, we change the diameter of tube and finally we can have optimum fluid linear velocity in the heat exchanger.

분산형 소형 연료전지용 1KW급 열교환기 설계 (Heat Exchanger Design For The Individually Allocated Fuel Cell For 1kw Power generation)

  • 이택홍;박태성;김태완;노재현;강영진
    • 한국수소및신에너지학회논문집
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    • 제25권1호
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    • pp.39-46
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    • 2014
  • Our lab designs a heat exchangers for hydrogen gas. Coolant is water, thus it is very difficult to determine heat transfer parameters in this gas-liquid system. Repeated experiments gives overdesign value 6.06%, overall heat transfer coefficient 36.32 ($kcal/m^2-hr-^{\circ}C$) for Hydrogen. Theoretically determined overall heat transfer coefficient is 38.44 ($kcal/m^2-hr-^{\circ}C$). Our lab simulated this system and overdesign 30.4% shows good match with this experiment by HTRI. These parameters are in same range with literature.

친수 표면처리 종류에 따른 공기 예열 열교환기의 응축 열전달 실험적 연구 (Experimental Study of Condensation Heat Transfer in Pre-heating Exchanger to the Type of Hydrophilic Surface Treatment)

  • 석성철;정태용;신동훈;황승식;최규홍;박재원
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2012년도 제45회 KOSCO SYMPOSIUM 초록집
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    • pp.237-238
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    • 2012
  • Recently, an energy-saving due to the energy utilisation efficiency enhancement is important. In order to improve the heat efficiency of the general residential boiler, We performed an experiment of condensation heat transfer to air pre-heat exchanger adhered to the condensing boiler. In this research, We analyze the heat transfer performance through the hydrophilic surface treatment(plasma, etching). The results of the research, On plasma and etching treated surface, Overall heat transfer coefficient is displayed the tendency to increase.

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